GB600118A - Improvements in or relating to the catalytic oxidation of hydrogen sulphide in gaseous mixtures - Google Patents
Improvements in or relating to the catalytic oxidation of hydrogen sulphide in gaseous mixturesInfo
- Publication number
- GB600118A GB600118A GB2880245A GB2880245A GB600118A GB 600118 A GB600118 A GB 600118A GB 2880245 A GB2880245 A GB 2880245A GB 2880245 A GB2880245 A GB 2880245A GB 600118 A GB600118 A GB 600118A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sulphur
- oxygen
- hydrogen sulphide
- sulphide
- temperatures
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/34—Purifying combustible gases containing carbon monoxide by catalytic conversion of impurities to more readily removable materials
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Catalysts (AREA)
Abstract
Gaseous mixtures, e.g. coal or fuel gas, are contacted in the presence of oxygen with a single solid catalyst mass comprising a sulphide or sulphides of nickel or cobalt at a temperature not exceeding 80 DEG C., but preferably above the dew point of the mixture, to oxidize the hydrogen sulphide content to sulphur. The process may be used to remove either hydrogen sulphide or oxygen. High humidity, e.g. 80-100 per cent of saturation and the addition of ammonia assist the reaction. Low temperatures and oxygen concentration reduce the tendency to side reactions leading to sulphur oxides. In examples, nickel or cobalt hydroxide or basic carbonate are treated with hydrogen sulphide at 100 DEG C. to produce the catalysts and temperatures of 25-27 DEG C. are used for the catalysis. Catalyst poisoned by sulphur or sulphate may be regenerated with a solvent, e.g. carbon disulphide, aromatic hydrocarbons or preferably ammonium sulphide or by removal of sulphur by evaporation or conversion, e.g. with hydrogen, to a gaseous compound. Oxygen may be added to the gas or adsorbed, e.g. from air on the catalyst prior to reaction, which allows countercurrent operation. According to the Provisional Specification, temperatures up to 250 DEG C. may be used, the catalysts may be produced by precipitation or by reduction of sulphates and may be used in gaseous suspension, on a carrier, or as a broken cake. Specifications 241,221, [Class 38 (v)], and 276,347, [Class 1 (i)], are referred to.
Publications (1)
Publication Number | Publication Date |
---|---|
GB600118A true GB600118A (en) | 1948-03-31 |
Family
ID=1741274
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2880245A Expired GB600118A (en) | 1945-10-30 | Improvements in or relating to the catalytic oxidation of hydrogen sulphide in gaseous mixtures |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB600118A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4311683A (en) * | 1976-06-28 | 1982-01-19 | Union Oil Company Of California | Process for removal of hydrogen sulfide from gas streams |
US4444741A (en) * | 1979-04-04 | 1984-04-24 | Union Oil Company Of California | Catalyst and process for oxidizing hydrogen sulfide |
US4444742A (en) * | 1979-04-04 | 1984-04-24 | Union Oil Company Of California | Catalyst and process for oxidizing hydrogen sulfide |
US4444908A (en) * | 1979-04-04 | 1984-04-24 | Union Oil Company Of California | Catalyst and process for oxidizing hydrogen sulfide |
US4528277A (en) * | 1979-04-04 | 1985-07-09 | Union Oil Company Of California | Catalyst for oxidizing hydrogen sulfide |
US4576814A (en) * | 1979-04-04 | 1986-03-18 | Union Oil Company Of California | Catalyst and process for oxidizing hydrogen sulfide |
-
1945
- 1945-10-30 GB GB2880245A patent/GB600118A/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4311683A (en) * | 1976-06-28 | 1982-01-19 | Union Oil Company Of California | Process for removal of hydrogen sulfide from gas streams |
US4444741A (en) * | 1979-04-04 | 1984-04-24 | Union Oil Company Of California | Catalyst and process for oxidizing hydrogen sulfide |
US4444742A (en) * | 1979-04-04 | 1984-04-24 | Union Oil Company Of California | Catalyst and process for oxidizing hydrogen sulfide |
US4444908A (en) * | 1979-04-04 | 1984-04-24 | Union Oil Company Of California | Catalyst and process for oxidizing hydrogen sulfide |
US4528277A (en) * | 1979-04-04 | 1985-07-09 | Union Oil Company Of California | Catalyst for oxidizing hydrogen sulfide |
US4576814A (en) * | 1979-04-04 | 1986-03-18 | Union Oil Company Of California | Catalyst and process for oxidizing hydrogen sulfide |
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